Strippable compositions comprising wax ethylene-vinyl acetate copolymer and polyglycol monoester



STRIPPABLE COMPOSITIONS COMPRISING WAX ETHYLENE-VINYL ACETATE COPOLYMER AND POLYGLYCOL MONOESTER Charles J. Kremer, Brookhaven, Pa., assignor to Atlantic Richfield Company, Philadelphia, Pa., a corporation of Pennsylvania N Drawing. Filed June 10, 1966, Ser. No. 556,573

Int. Cl. C09d 5/20; C08h 9/10 US. Cl. 26027 17 Claims ABSTRACT OF THE DISCLOSURE Strippable wax coatings comprising a wax, an ethylene vinyl acetate copolymer and a mono or poly (oxyalkylene) glycol mono-fatty acid ester are disclosed. A preferred ester is poly (ethoxy) glycol mono-stearate. A plasticizer and/ or a hydrocarbon oil can also be added to the compositions if desired.

This invention relates to strippable wax coating compositions. In another aspect, it relates to articles of manufacture wherein at least a portion of the surface is coated with this strippable wax composition.

Strippable coatings are well-known in the art. They are utilized in applications wherein it is desirable to provide temporary surface protection against abrasion, rust, dirt and other damage occurring in storage and handling. After the necessary protection period has expired, it is desirable that these coatings be removed with a minimum of time and effort. These requirements have led to the development of various compositions which may be deposited as coatings upon a surface and thereafter removed as essentially continuous films. For example, polyvinyl chloride plastisols can be deposited, cured, and then peeled from a surface. This coating is very expensive and therefore, can only be economically deposited in thicknesses of a few mils. Furthermore, a strippable coating is produced only after the liquid plastisol has been properly cured at temperatures in the order of 300 F.

In order to eliminate the necessity of a cure, hot melt coatings have been produced from cellulosic materials such as ethyl cellulose in combination with large proportions of mineral oil. These compositions usually are quite odorous, have oily surface appearances and require coating temperatures in excess of 300 F. Other hot melt coatings such as those made from wax alone are not strippable. The addition of the various polymers including ethylene-vinyl acetate copolymers imparts physical strength to the wax film but it also increases the adhesive bond between the surface and the film. In order to impart strippability, various additives such as mineral oil, flu-orinated compounds, silicones and partial esters have been incorporated into these wax-polymer compositions. These additives either impart high cost, poor coating appearance or necessitate extensive coating techniques.

It has now been found that outstanding strippable coatings can be produced by combining wax with ethylenevinyl acetate copolymers and minor amounts of a mono or poly (oxyalkylene) glycol mono fatty acid ester. These compositions offer excellent strippability, low cost and they do not require complex coating processes. The coat- United States Patent 0 'ice ing compositions of this invention can be economically applied in considerable thicknesses using a hot melt technique without need of any subsequent cure.

The compositions of this invention may be used to protect the surfaces of metals such as aluminum, steel, zinc, brass, and chromium or the surfaces of various plastic or synthetic products such as laminates of phenol-formaldehyde, melamine-formaldehyde and urea/formaldehyde resins, phonograph records, and the surfaces of many natural products such as wood paneling, flooring strips and the like. In general, the compositions of this invention may be utilized on any solid surface such as glass, ceramic or mica which forms a minimum adhesive bond with the coating.

It is an object of this invention to provide wax compositions which may be deposited upon a surface and thereafter completely removed from the surface as essentially continuous films.

It is a further object of this invention to provide articles of manufacture which have these strippable wax compositions deposited upon their surfaces.

The compositions of this invention comprise in parts by weight:

(A) parts of wax; and (B) from 10 to 300 parts of a polymeric composition consisting essentially of- (i) from 40l00 weight percent of an ethylene-vinyl acetate copolymer having a vinyl acetate content ranging from 15-35 weight percent, and

(ii) from 060 weight percent of a plasticizer for the ethylene-vinyl acetate copolymer;

(C) a mono or poly (oxyalkylene) glycol mono fatty acid ester in an amount suflicient to impart strippability;

(D) from 0 to 20 parts of a hydrocarbon oil having a viscosity at 210 F. in excess of 25 SSU.

The mono or poly(oxyalkylene) glycol mono fatty acid esters hereafter described broadly as esters must be present in the compositions within a certain critical concentration range. The concentration must be sufficient to impart strippability without completely destroying the bond between the surface and the coating. In order to be considered strippable, it is necessary that the coating be capable of being totally removed from the surface as essentially continuous films. These critical ester concentrations are dependent upon the type of ester utilized, the type and amount of other components present, and the degree of strippability desired. In most compositions, strippability is obtained with ester concentrations as low as 0.5 part by weight in 100 parts wax. Concentrations which range from 1 to 5 parts by weight per 100 parts Wax have been found to be most satisfactory. Higher concentrations, while operable, are accompanied by substantial ester migration to the surface of the coating. The extent of migration varies with the particular ester and in general is related to its wax compatibility. This migration may totally destroy the adhesive bond, or provide an unattractive coating appearance and feel.

The mono or poly (oxyalkylene) glycol mono fatty acid esters which can be utilized in the practice of this invention have the following structural formula:

wherein R is an aliphatic radical containing 30 carbon atoms, X is the alkoxy radical, y is an integer from 1 to the quotient of 1320 divided by the molecular weight of X, and W is hydrogen or a lower alkyl radical containing up to about 6 carbon atoms.

R is an aliphatic radical containing 103O carbon atoms, and can be saturated or unsaturated, and linear or branched chain. It may be derived from the hydrocarbon residues of monocarboxylic fatty acids. These hydrocarbon residues can be substituted with a pendant oxygen atom as a keto or hydroxyl group or an ester linkage. Suitable hydrocarbon residues which can be utilized include but are not limited to the residues derived from saturated acids such as n-undecylic, lauric, myristic, npentadecylic, palmitic, margaric, stcaric, avachidic, behenic, lignoceric, cerotic, n-heptacosoic and n-hentriacontoic; unsaturated acids such as the mono-ethenoid, caproleic, IO-decylenic, lauroleic, palmitoleic, oleic, elaidic, erucic, selacholeic and lumegueic acids; the polyethenoid acids such as linolelaidic, eleostearic, punicic, linolenic and moroetic acids; substituted acids such as ricinoleic, lanoceric and licanic acids; branched chain acids such as Z-methyl-dodecanoic, l4-ethyl hexadecanoic, l8-n-propyl heneicosanoic, Z-methyl tetracosanoic, 9- oxtyl heptadecanoic, 3,3-dimethyloctadecanoic and 2,9- dirnethyl-octadecanoic acids; and from naturally occurring acid mixtures such as coconut and soybean oil and tallow. Preferably R is a linear, unsubstituted aliphatic radical containing 10-17 carbon atoms. More preferably, R is the hydrocarbon residue derived from stearic acid having the formula (C17H35-).

X represents the alkoxylated portion of the molecule and is a radical having the structural formula:

TABLE A When n is and n is R is and R is 0 2 CH3 H l 0 l 1 CH; H

or CzHa H 01 CH3 CH 1 2 CH and H H 2 O t. H 2 1 CH; H 3 0 4 O Preferably, the alkoxy radical is derived from ethylene oxide or propylene oxide. Most preferably, it is derived from ethylene oxide.

The alkoxy chains which are included in the above formula include the methoxy chain; chains derived from 1,2-epoxides such as ethylene, propylene, butylene, and isobutylene oxides; chains derived from the l,3-epoxides such as 1,3-propylene, butylene, and isobutylene oxides;

chains derived from the 2,3-epoxides such as 2,3-butylene oxide; and chains derived from the 1,4-epoxide such as tetrahydrofuran.

In general, the length of the alkoxy chain as defined by y is determined by its molecular weight. It has been found that the marginal strippability is attained when the molecular weight of the alkoxy chain exceeds 1320. Therefore, y can range from 1 to the quotient of 1320 divided by the molecular weight of X. Preferably, y ranges from 1 to 25 and most preferably from ll0.

The range of value of y for the designated alkoxy radical is set forth in Table B. The maximum values were calculated from the formula: Y=l320 divided by the molecular weight of X. The maximum values were calculated for chains wherein a single type of alkoxy radical was utilized. However, individual chains having mixtures of the various alkoxy radicals can be prepared and the maximum value of y determined after defining the actual number of each type of alkoxyl radical present in the chain.

Where the alkoxy y is an integer radical isranging from Methoxy l-44 Ethoxy l-30 Propoxy l22 Butoxy l-18 Specific mono or poly (oxyalkylene) glycol mono fatty acid esters which can be utilized in the practice of this invention includes but is not limited to:

poly (oxyethylene) glycol mono decanoate poly (oxymethylene) glycol mono-6-methyl-lO-undecenoate poly (oxytrimethylene) glycol mono tetradecanoate poly (oxy-l,3-butylene) glycol mono 4,4-dimethyl-9- dodecenoate poly (oxyethylene) glycol mono hexadecanoate oxypropylene glycol mono-4-pentyl-lO-undecenoate poly (oxyrnethylene-oxy-1,3-butylene) glycol mono-l2- hexadecenoate poly (oxyethylene) glycol octadecanoate poly (oxytetramethylene) glycol mono-l4-octadecenoate poly (oxyethylene) glycol mono-l2-octadecynoate poly (oxypropylene) glycol mono-[i-decanoate-n-octanoate poly (oxy-Z-butylene) glycol mono octadecanoate poly (oxyethylene-oxypropylene) glycol mono-3,6,9-tripropylundecanoate poly (oxy-2-butylene) glycol mono-12,16-eicosenoate poly (oxymethylene) glycol mono-7,11-dioxo-docosanoate oxyethylene glycol mono-9-nonyl-IZ-pentadecenoate poly (oxypropylene-oxytrimethylene) glycol mono-6- hydroxyl S-hexacosenoate poly (oxytetramethylene) glycol mono-11,18-diethyltetracosanoate poly (oxyethylene) glycol mono triacontanoate.

The preparation of these mono or poly (oxyalkylene) glycol mono fatty acid esters is not critical to the practice of this invention. For example, these compounds can be prepared by reacting an aliphatic fatty acid, acid chloride, or ester with a mono or poly (oxyalkylene) glycol. Specifically, the most preferred release agent, poly (oxyethylene) glycol mono stearate can be prepared by reacting stearic acid with poly (oxyethylene) glycol.

In the above alkoxylated compounds wherein it is desirable to utilize the methoxy linkage, it is necessary to first react at least one molecule of ethylene oxide or a higher alkylene oxide to establish a basic medium for the propagation of the methoxy group. Once this basic medium has been established, formaldehyde or its dimers and trimers may be reacted to promulgate the methoxylated chain. It is necessary, however, to cap these methoxylated chains in order to provide stability. This requires that the terminal hydrogen on each methoxy be removed and replaced by any suitable capping radical. For example, this terminal OH group can be esterified with methyl iodine to form an (OCH group.

The wax component of this invention can be any wax which can be deposited upon a surface as a molten or solvent cut coating and thereafter changed into a solid phase by cooling or by evaporation of the solvent. These waxes can be of mineral, vegetable, animal or synthetic origin. Mixtures of various waxes can also be utilized. Exemplary of waxes having a mineral origin are the petroleum and hydrocarbon waxes such as paraffin, microcrystalline, slack, ozocerite and montan waxes. Waxes having a vegetable origin are carnauba, candelilla, Japan waxes and the like. Waxes having an animal origin include bees, Chinese, insect and similar waxes. In the animal and vegetable waxes the main constituents are high molecular weight esters and saturated hydrocarbons and lesser amounts of alcohols and acids. Exemplary of the synthetic waxes include those produced by the esterification of polyhydric alcohols or by the hydrogenation of vegetable oils or those made by the Fischer-Tropsch synthesis or substituted waxes such as oxidized or chlorinated polyethylene wax.

The use of petroleum waxes represents a preferred embodiment of this invention. These waxes include paraffin waxes which have a melting point from about 115 F. to about 200 F. and the microcrystalline waxes having a melting point from about 140 F. to about 210 F. These waxes may be fully refined and thus contain very small amounts of hydrocarbon oils or they may be semirefined (slack waxes) and have hydrocarbon oil contents of up to about 30 percent. As more fully discussed hereafter, oils of this type may be added to the compositions of this invention to enhance the strippability of the coating in amounts ranging up to percent of the total composition. Therefore, in determining an upper oil loading, the amount which is present due to the addition of a semi-refined wax should be included.

The most preferred compositions of this invention utilize 100 percent by weight microcrystalline wax having a melting point ranging from 140 F. to 210 F. or a combination of petroleum waxes comprising from 20 to 80 percent by weight of a paraffin wax having a melting point ranging from 120 F. to 180 F. and from 80 to 20 percent of microcrystalline wax having a melting range from about 140 F. to about 210 F. This wax mixture provides strippable coating which can be utilized in high temperature applications. Increasing the concentration of microcrystalline wax will impart a higher maximum use temperature and improve the ultimate physical strength while decreasing dimensional stability. With respect to paraffin waxes as a class the use of a non-normal paraffin wax imparts higher physical strength than the normal base parafi'ln waxes.

The copolymers which can be utilized in the practice of this invention are solid thermoplastic polymers produced by polymerizing a major amount of ethylene with a minor amount of vinyl acetate. These copolymers should be solid at ambient temperatures (i.e. 70 F.) and have a molecular weight sufficient to impart film strength without requiring excessive copolymer concentrations. The molecular weight can be further defined through the term melt index as determined by ASTM D-1238-62. In general, the operable copolymers have melt indexes of less than 500. Preferably, the melt index is less than and most preferably, less than 5. Copolymers having melt indexes as low as .5 have been prepared in the laboratory and have been found to impart outstanding strength characteristics. The vinyl acetate concentration in the copolymers can range from 15 to percent by weight. The higher concentration defines the practical limits of copolymer compatibility with the wax. Copolymers having a vinyl acetate content of less than 15 percent are more compatible but excessive copolymer concentrations are necessary to impart the desired film properties. The optimum film properties are obtained with copolymers having a vinyl acetate concentration ranging from 25 to 30 weight percent and are therefore preferred in the compositions of this invention.

The ethylene-vinyl acetate copolymers can be utilized in the practice of this invention alone or in conjunction with a compound which is a plasticizer for the copolymer. Exemplary compounds which are recognized as plasticizers for ethylene-vinyl acetate copolymers include but are not limited to monomeric plasticizers such as dioctyl adipate, dioctyl, dioctyl phthalate, butyl phthalyl glycollate and aceto tributyl citrate or higher molecular weight plasticizers such as polyterpenes, polybutenes, epoxidized soybean oil, coumarone-indene resins, polystyrene and organic carboxylic acids. These plasticizers in general have molecular weights of less than 3,000, are compatible with wax at the blending and application temperatures and have boiling or degradation temperatures which are higher than the temperatures incurred during coating. The coumarone-indene resins represent a preferred class of plasticizers. They are prepared by the catalytic polymerization of coal-tar, light-oil fractions boiling between 150 C. and 200 C. This fraction is commonly called crude heavy solvent and contains primarily indene, styrene, cyclopentadiene and their methyl homologs and minor amounts of coumarone. These resins have a softening point of less than C. as determined by the ring and ball method described in ASTM Test Number D3662T. Preferably, this softening point is less than 50 C.

The use of organic carboxylic acids is plasticizers for the ethylene-vinyl acetate copolymers also represents a preferred embodiment in this invention. This carboxylic acid must be wax compatible, have an acid number in excess of about 20 and a molecular weight ranging from to 3,000. Preferably, the acid number is in excess of 30. Compounds with low acid numbers and high molecular weights, i.e., oxidized polyethylene are not desirable because they increase the viscosity of the molten composition without imparting the desired properties. Any aliphatic, acyclic or aromatic acid having one or more carboxyl groups can be utilized. For example, dimerized and trimerized fatty acids, rosin acids and naphthoic acids can be also utilized.

The ethylene-vinyl acetate copolymer should be utilized in amounts sufficient to impart physical strength to the coating thus allowing them to be stripped from the surface as essentially continuous films. This requires a proper balance between the adhesive and cohesive forces'with the adhesive force being less than the cohesive force. As the concentration of copolymer is increased, the physical strength of film is also increased. However, accompanying this improvement, is an increase in melt viscosity and in processing and material costs. Therefore, from both economic and processing viewpoints, the copolymer concentration should be the optimum required to impart the necessary strippability. A portion of the ethylenevinyl acetate copolymer can be replaced by the plasticizers heretofore described. This copolymer-plasticizer mixture is hereafter described in the specification and claims as the polymeric composition. This composition consists essentially of from 40 to 100 percent by weight of an ethylene-vinyl acetate copolymer and from 0 to 60 percent by weight plasticizer. Most preferably, the plasticizer concentration ranges from 5 to 30 percent. The amount of polymeric composition which can be utilized in the compositions of this invention can range in amounts from 10 parts to 300 parts by weight of wax. Therefore, the copolymer can range in concentrations of from 4 to 300 parts per 100 parts of wax, and the plasticizer concentration can range from 0 to 180 parts per 100 parts wax. When the maximum plasticizer concentration of 180 parts is utilized, the maximum copolymer concentration is 120 parts. The most preferred concentration of polymeric composition ranges from to 110 parts per 100 parts of wax.

As previously stated, a hydrocarbon oil can be added to the composition of this invention to aid in strippability, impart a plasticizing effect and lower the hot melt viscosity. This hydrocarbon oil has a viscosity at 210 F. of greater than SSU and preferably from about to about 500 SSU at 210 F. A preferred oil is a highly refined n-paraffin petroleum oil having a viscosity of from 43 to SSU at 210 F. The oils can be incorporated into the compositions of this invention in amounts ranging up to about 20 parts per 100 parts Wax. However, excessive oil loading will greatly reduce tensile strength. Preferably, the oil concentration ranges up to about 15 parts and most preferably from 1 to 10 parts. As previously stated, some petroleum waxes commonly known as semi-refined waxes contain substantial amounts of oil. When these semi-refined waxes are utilized in this invention, its oil content should be taken into account in determining the maximum or optimum oil loading. In determining the amount of wax present for the purposes of defining a common parts basis, the inherent oil content of semi-refined wax should be excluded.

Ingredients commonly added to wax or ethylene-vinyl acetate copolymers can be incorporated into the compositions of this invention in functional amounts without departing from the scope thereof. Examples of these ingredients include but are not limited to: heat and ultraviolet stabilizers, inert fillers, secondary plasticizers, antiblocking agents, pigments and colorants, anti-oxidants, gloss stabilizers, viscosity-index improvers, solvents, antiscuff agents, etc.

The preparation of the compositions of this invention is not critical to the practice thereof and can be conducted under any suitable method. For example, these compositions can be prepared by heating the wax to a. temperature above its melting point, adding the ethylenevinyl acetate copolymer, release agent and other additives and agitating vigorously until a homogenous hot melt is obtained.

When a plasticizer is utilized, it is preferable to incorporate the plasticizer into the melted wax prior to the addition of the copolymer in order to facilitate the dispersion of the copolymer. Similarly, a coating composition can be prepared by combining ingredients with a common solvent or by suspending them in a non-solvent liquid such as water. A specific method for preparation is as follows: The waxes are melted together, any antioxidants or heat stabilizers are added and the melt is then brought to a temperature above about 275 F. The plasticizer, if it is not free flowing is heated to about 275 F. and then added to the hot melt. The ethylenevinyl acetate copolymer is then added to the melt accompanied by vigorous stirring while maintaing the melt temperature above about 275 F. After all of the copolymer has been added, the melt temperature is raised to about 300 F. and agitated until the copolymer and resins are completely dispersed. The desired release agents are then added.

Articles of manufacture can be prepared in any manner which results in a deposition of coating on its surface. For example, the articles may be dipped in a hot melt and cooled to allow the coating to solidify. This coating can also be deposited utilizing common coating processes such as curtain coating, roll coating and spray coating. The same technique is followed when the solvent or suspended wax system is utilized. After coating, the solvent or carrier is evaporated. These coatings may be applied in any thickness. However, it is necessary that the thickness provide sufficient strength in the film to allow the film to remain intact during stripping. Normally, coating thicknesses greater than 1 mil. have this requisite strength.

The following examples are given to illustrate the preferred embodiments of this invention and should not be construed as limitations upon the invention. All parts are by weight.

EXAMPLE I The waxes of Table I were melted together and 20 ppm. of 4,4 methylene bis(2,6 di tert butyl phenol) was added as a stabilizer. The coumarone-indene resin was heated to 275 F. and then added to the hot melt. The ethylene-vinyl acetate copolymer was then added to the melt with constant and vigorous agitation while maintaining a melt temperature above 275 F. The melt temperature was raised to 300 F. after all of the copolymer had been added and maintained at that temperain re for approximately 5 minutes until all of the copolymer had dissolved. The melt temperature was then lowered to 280 F. and the various release agents were added. The hot melt was deposited with a coating bar as 1 to 5 mil. coatings on glass surfaces. The coating was allowed to cool to room temperature and after a 24 hour period, its strippability was evaluated. The results are reported in 4 different categories:

Excellent (E) is used to designate a coating which could be easily and rapidly removed as a single continuous film. Good (G) denotes a coating which could be easily removed without the application of excessive force. However, at faster stripping rates it had a propensity to tear in random fashion along the direction of the force and thus was removed as several large pieces. Fair (F) designates a coating which could be stripped only by applying excessive force. Slow removal rates were necessary and even then it came oif in the for-m of small random pieces. Poor (P) denotes a coating which had high adhesion requiring the application of excessive force at very slow removal rates. Very small random pieces were obtained under these conditions. Not Strippable (N.S.) means that the coating did not exhibit any stripping characteristics.

TABLE I Formulation N o 1 2 3 Wax 1 100 100 Ethylene-vinyl acetate copylorner 42 42 42 Coumarone-indene resin 16. 1 l6. 1 16. 1 Hydrocarbon oil 4 3. 2 3. 2 6. 6 Poly (oxyethylene) glycolmono-stearate 0 1. 6 0 Stnppabillty properties:

24 hours after cooling to 70 F F E F to P After heating coating to 170 F. for 10 minutes and then cooling to 70 F. for 24 hours E P 1 The wax was a blend of 70.5 parts mierocrystalline wax having a melting point of 1 75 F. (ASIM D-l27) and 29.5 parts of a fully refined paramn wax having a melting point ranging from 150 to 155 F. (ASTM- D-87). Both waxes had an oil content of less than 1 percent.

2 An ethylene-vinyl acetate copolyrner having a bound vinyl-acetate content of 28 percent; by weight and a melt index of 3.0 (ASTM D-l238-57T).

3 Goumarone-mdene resin having a ring and ball softening point 0! 38 C. (ASTM D-36-627).

t A solvent refined hydrocarbon oil comprised mainly of n-paraflins ggyllg a viscosity index of to and a viscosity at 210 F. of 43-46 6 With reference to the general formula set forth in the specification, the poly(oxyethylene) glycol mono stearate is defined as follows: R is C11Hs5, X is ethoxy, 11:10 and W is hydrogen.

Table I demonstrates that the addition of a poly(oxyethylene) glycol mono-stearate to the prior art compositions greatly enhances the strippability. By comparing Formulation 3 with 2, it is demonstrated that even higher amounts of the prior art stripping agents (oil) will not impart this outstanding strippability.

EXAMPLE II The compositions of Table II were prepared and evaluaged in accordance with the methods set forth in Examp e I.

TAB LE 11 Formulation No 4 5 6 7 8 9 Wax 1 100 100 100 100 100 100. Ethylene-vinyl acetate copolymer 50 50 50 50 50 50. Styrene Polymer 8 8 8 8 8 Rosin Acids l 40 40 40 40 40 25. Release Agent:

Type Poly (oxyethylene) Poly (oxyethylene) Poly (oxyglycol mono coconut glycol mono rosin ethylene) acid ester 5 acid ester glycol mono stearate. 7 1.0 2.0 1.0 2.0 2.5.

NS F G P P E.

l The wax component contained 80 parts of a microcrystalline wax having a melting point of 175 F. (ASTM D-l27) and 20 parts of a refined paraffin wax having a melting point of 150155 F. (ASTM D-87). Both waxes had an oil content of less than 1 percent. 2 As defined in Table I, footnote 2.

3 A liquid polystyrene homopolymer having an average molecular weight of 325 to 350, a viscosity at 100 F. of 1500 SSU, and an initial boiling point oi 310 F. at 7 mm. of mercury pressure.

A high degree of disproportionated wood rosin, melting point of 181 F. (ring and ball), acid number of 154,

saponifieation number of 189.

5 With reference to the general formula in the specification, R is ablend of fatty acid esters derived from coconut oil containing approximately percent by weight C10 ,50 percent 012, percent C14, 10 percent C15. 5 percent 019-020; X is ethoxy, W is hydrogen and y is 15.

6 With reference to the general formula in the specification, R is the fatty residue of abietic acid; X is ethoxy;

W is hydrogen and y is 15.

7 As defined in Table I, footnote 5.

It is apparent from Table II that the coconut oil derived poly (ethoxylated) mono fatty acid ester i-mparts strippability to prior art non-strippable composition.

It should also be noted that the poly (ethoxylated) nonfatty acid ester does impart this strippability. (Compare Formulation Nos. 7 and 8.)

EXAMPLE III In order to demonstrate the effect of plasticizers, blends containing:

Parts Wax 100 Ethylene-vinyl acetate copolymer 81.8 Plasticizer 45.5

were prepared in accordance with the method set forth in Example I. The wax component contained percent by weight microcrystalline wax having a melting point of 175 F. (ASTM ED-127) and 75 percent by weight of a paraffin wax having a melting point of 135 F. (ASTM D-87). The ethylene-vinyl acetate copolymer 28 percent by weight bound vinyl acetate and had a melt index. of 3.0 (ASTM D-1238-57T).

The various plasticizers and their evaluations are set forth in Table III.

wherein R' is a methyl, ethyl or hydrogen radical; R" is a methyl or hydrogen radical; and n and n are corresponding integers which define X as an alkoxy radical having from l-4 carbon atoms derived from aldehyde, oxirane, oxetane or tetrahydro- TABLE III Formulation No 10 11 12 13 14 15 is t P 2 Coumarone- Dioctyl Dioctyl Epoxidized Polybutenefi P S mlzer 01y terpene indene adipate. phthalate. soybean oil 4 resin. 3

Hot melt vis. at 300 F., cp 6,425 6,300 3,350 4,280 5,750 4, 250. Elongation, percent 1 u 166 16"... 36 45 33.

Energy absorption 1 factor, it.lbs./cu. in-- 25.4 52.2 4.4 1 6 l5. 1 l. 10

1 Microtensile method, ASTM D-1708-59T.

D zffizrrgene resin having a ring and ball softening point of C. (ASTM 7 l B As defined in footnote 3, Table I.

The energy absorption factor is the area under the curve obtained by plotting the force applied on the com position (stress) against its resulting elongation (strain). Thus, the higher energy absorption factors described compositions which in the presence of a release agent can be readily stripped without tearing. In this regard, the composition plasticized with the coumarone-indene resin has the most outstanding elongation and energ absorption characteristics.

I claim:

1. A composition comprising in parts by weight:

(A) 100 parts of wax;

(B) from 10 to 300 parts of a polymeric composition consisting essentially of [i] from 40-95 weight percent of an ethylenevinyl acetate copolymer wherein the vinyl acetate content ranges from 15-35 weight percent 65 wax is a petroleum wax.

3. A composition according to claim 2 wherein the petroleum wax is a mixture comprising of from 20-80 weight percent paraflin wax and from 80-20 weight percent microcrystalline wax.

4. A composition according to claim 1 wherein the polymeric composition is present in an amount ranging from 20-110 parts.

5. A composition according to claim 1 wherein the ethylene-vinyl acetate copolymer has a vinyl acetate con- 1 1 tent ranging from 25-30 weight percent and a melt index of less than 25.

6. A composition according to claim 1 wherein the plasticizer is present in an amount ranging from 5-30 weight percent by weight of the polymeric composition.

7. A composition according to claim 1 wherein the plasticizer is a coumarone-indene resin, having a softening point of less than 50 C.

8. A composition according to claim 1 wherein the plasticizer is a Wax compatible organic carboxylic acid having an acid number in excess of 20 and a molecular weight ranging from 150 to 3,000.

9. A composition according to claim 8 wherein the organic carboxylic acid is abietic acid.

10. A composition according to claim 1 wherein the hydrocarbon oil of part (D) is present in an amount ranging from 4-10 parts and has a viscosity of 210 F. ranging from 35-500 SSU.

11. A composition according to claim 1 wherein the poly (oxyalkylene) glycol mono fatty acid esters of part 16. An article of manufacture comprising a solid object having at least a portion of its surface coated with the composition of claim 1.

17. A composition according to claim 1 wherein the value of y in the fatty acid ester ranges from 10 to 15.

References Cited UNITED STATES PATENTS 3,207,716 9/ 1965 Lippoldt 260-23 3,294,722 12/1966 Apikos et al 260-28.5 3,321,427 5/1967 Tyran 26028.5 3,322,709 5/1967 Hammer 260-28.5 3,325,431 6/1967 McManus 26028.5 3,329,642 7/1967 Lima et a1 260-31.4

OTHER REFERENCES KirkOthmer, Encyclopedia of Chemical Technology, vol. 7, 1951, pp. 258, 260, 261.

DONALD E. CZAJA, Primary Examiner.

R. A. WHITE, Assistant Examiner.

US. Cl. X.R. 

